JPS53129176A - Catalytic reaction method of reducing gas and high pressure reactor for carrying out said method - Google Patents
Catalytic reaction method of reducing gas and high pressure reactor for carrying out said methodInfo
- Publication number
- JPS53129176A JPS53129176A JP2672478A JP2672478A JPS53129176A JP S53129176 A JPS53129176 A JP S53129176A JP 2672478 A JP2672478 A JP 2672478A JP 2672478 A JP2672478 A JP 2672478A JP S53129176 A JPS53129176 A JP S53129176A
- Authority
- JP
- Japan
- Prior art keywords
- carrying
- high pressure
- reducing gas
- catalytic reaction
- pressure reactor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title 2
- 238000006555 catalytic reaction Methods 0.000 title 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
- C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0005—Catalytic processes under superatmospheric pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0405—Apparatus
- C07C1/042—Temperature controlling devices; Heat exchangers
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- General Health & Medical Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Pressure Vessels And Lids Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2717101.3 | 1977-04-18 | ||
DE2717101A DE2717101C2 (en) | 1977-04-18 | 1977-04-18 | Process for the catalytic conversion of a reducing gas |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS53129176A true JPS53129176A (en) | 1978-11-10 |
JPS6022968B2 JPS6022968B2 (en) | 1985-06-05 |
Family
ID=6006559
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP53026724A Expired JPS6022968B2 (en) | 1977-04-18 | 1978-03-10 | Method for catalytic reaction of reducing gases and high pressure reactor for carrying out this method |
Country Status (4)
Country | Link |
---|---|
US (1) | US4259312A (en) |
JP (1) | JPS6022968B2 (en) |
AU (1) | AU521097B2 (en) |
DE (1) | DE2717101C2 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3430870A1 (en) * | 1984-08-22 | 1986-02-27 | Didier Engineering Gmbh, 4300 Essen | METHOD FOR EXHAUST GAS PURIFICATION |
DE3430886A1 (en) * | 1984-08-22 | 1986-02-27 | Didier Engineering Gmbh, 4300 Essen | CATALYST FOR SEPARATING NITROGEN OXIDES FROM COMBUSTION EXHAUST GASES |
DE3430887A1 (en) * | 1984-08-22 | 1986-02-27 | Didier-Werke Ag, 6200 Wiesbaden | METHOD FOR REACTIVATING A CATALYST AND SYSTEM FOR CARRYING OUT THE METHOD |
DE3516359C1 (en) * | 1985-05-07 | 1986-12-04 | Didier Engineering Gmbh, 4300 Essen | Process for the removal of nitrogen oxides and soot from exhaust gases from heavy oil machines or heavy oil furnaces |
DE3532207A1 (en) * | 1985-09-10 | 1987-03-19 | Didier Eng | METHOD FOR PRODUCING CATALYST SHAPES |
US5840259A (en) * | 1993-04-05 | 1998-11-24 | Catalytic Distillation Technologies | Boiling point reactor with heat removal |
US6432368B1 (en) * | 1994-06-30 | 2002-08-13 | General Electric Company | Staged catalytic ammonia decomposition in integrated gasification combined cycle systems |
US6641625B1 (en) | 1999-05-03 | 2003-11-04 | Nuvera Fuel Cells, Inc. | Integrated hydrocarbon reforming system and controls |
US7507384B2 (en) * | 2002-06-13 | 2009-03-24 | Nuvera Fuel Cells, Inc. | Preferential oxidation reactor temperature regulation |
CN106861559A (en) * | 2015-12-14 | 2017-06-20 | 江苏氢阳能源有限公司 | For the reactor of catalyzed endothermic reaction more than two-phase and two-phase |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR35077E (en) * | 1926-03-31 | 1929-12-10 | ||
BE366454A (en) * | 1928-12-31 | |||
DE973995C (en) * | 1951-08-03 | 1960-08-11 | Metallgesellschaft Ag | Process for utilizing the heat of reaction in the synthesis of ammonia or in other catalytic gas reactions |
AT215436B (en) * | 1959-06-24 | 1961-06-12 | Chemie Linz Ag | Process for conducting gas in catalytic high-pressure synthesis plants and device for carrying out the process |
DE1252184B (en) * | 1964-02-10 | 1967-10-19 | Badische Anilin- 6λ Soda-Fabrik Aktiengesellschaft, Ludwigshafen/Rhein | Process for the catalytic conversion of carbon monoxide with steam under pressure |
US3479298A (en) * | 1964-08-04 | 1969-11-18 | Lummus Co | Production of hydrogen |
US3498752A (en) * | 1966-10-26 | 1970-03-03 | Chemical Construction Corp | Apparatus for exothermic catalytic reactions |
GB1307845A (en) * | 1969-05-28 | 1973-02-21 | Ici Ltd | Reactor |
US3663179A (en) * | 1970-04-20 | 1972-05-16 | Chemical Construction Corp | Apparatus for exothermic catalytic reactions |
US3751232A (en) * | 1971-01-14 | 1973-08-07 | Universal Oil Prod Co | Means for effecting a multiple stage contact of a reactant stream |
US3807963A (en) * | 1972-03-09 | 1974-04-30 | J Smith | Reaction apparatus |
DE2427530C2 (en) * | 1974-06-07 | 1984-04-05 | Metallgesellschaft Ag, 6000 Frankfurt | Methanation reactor |
US4152407A (en) * | 1977-02-02 | 1979-05-01 | Warren Fuchs | Process and apparatus for exothermic reactions |
-
1977
- 1977-04-18 DE DE2717101A patent/DE2717101C2/en not_active Expired
-
1978
- 1978-03-10 JP JP53026724A patent/JPS6022968B2/en not_active Expired
- 1978-04-17 AU AU35149/78A patent/AU521097B2/en not_active Expired
-
1979
- 1979-10-03 US US06/081,615 patent/US4259312A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
AU521097B2 (en) | 1982-03-18 |
JPS6022968B2 (en) | 1985-06-05 |
DE2717101A1 (en) | 1978-10-26 |
AU3514978A (en) | 1979-10-25 |
US4259312A (en) | 1981-03-31 |
DE2717101C2 (en) | 1986-04-03 |
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